CN204503036U - Compound interleave cloth liquid reactor - Google Patents
Compound interleave cloth liquid reactor Download PDFInfo
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- CN204503036U CN204503036U CN201520130886.1U CN201520130886U CN204503036U CN 204503036 U CN204503036 U CN 204503036U CN 201520130886 U CN201520130886 U CN 201520130886U CN 204503036 U CN204503036 U CN 204503036U
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- reactant
- cylindrical shell
- pan feeding
- interleave
- compound interleave
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Abstract
The utility model provides a kind of compound interleave cloth liquid reactor, comprises cylindrical shell, it is characterized in that, be provided with compound interleave liquid distributor in described cylindrical shell; Described compound interleave liquid distributor comprises: at least 2 reactant pan feeding pipelines, each reactant pan feeding pipeline is communicated with some laterals, together with the lateral of each reactant pan feeding pipeline is arranged evenly with the lateral interleaved of other reactant pan feeding pipeline, each lateral is distributed with some apertures; The mouth of pipe of all reactant pan feeding pipelines all stretches out outside cylindrical shell.The compound interleave cloth liquid reactor that the utility model provides, owing to being provided with compound interleave liquid distributor in cylindrical shell, this compound interleave liquid distributor not only increases cloth liquid zone, and the alternate alternately cloth of reaction liquid is gone out, the instantaneous reactant liquor that just can make fully mixes, thus shorten incorporation time, thus make reaction more abundant, improve the production efficiency of product.
Description
Technical field
The utility model relates to mechanical field, particularly relates to a kind of compound interleave cloth liquid reactor.
Background technology
At chemical field, two or more liquid phase or gaseous reactant is usually needed to put into reactor, add the catalyst of solid granular simultaneously, under the effect that agitator stirs, liquid phase reactor thing is mixed, make granular catalyst be suspended in reactant equably simultaneously, thus make reaction more abundant, improve the productive rate of product.But, in the production process of reality, often abundant not owing to stirring, therefore, the purity of product is not high, productive rate is low, and in order to improve the productive rate of product, a time can only be spent more before the reaction the reactant in reactor and catalyst are stirred fully, so improve the productive rate of product, and although this measure improves the productive rate of product, reduce the production efficiency of product.
Utility model content
The purpose of this utility model is the defect solving the existence of above-mentioned prior art, provides a kind of productive rate that namely can ensure product, can ensure again the compound interleave cloth liquid reactor of the production efficiency of product.
A kind of compound interleave cloth liquid reactor, comprises cylindrical shell, it is characterized in that, be provided with compound interleave liquid distributor in described cylindrical shell;
Described compound interleave liquid distributor comprises: at least 2 reactant pan feeding pipelines, each reactant pan feeding pipeline is communicated with some laterals, together with the lateral of each reactant pan feeding pipeline is arranged evenly with the lateral interleaved of other reactant pan feeding pipeline, each lateral is distributed with some apertures;
The mouth of pipe of all reactant pan feeding pipelines all stretches out outside cylindrical shell.
Further, compound interleave cloth liquid reactor as above, comprise 2 reactant pan feeding pipelines circularized, be respectively circulating line, lower circulating line, upper circulating line is communicated with some top sets pipe, be communicated with some inferior division pipes at lower circulating line, described top set pipe and inferior division pipe interleaved are distributed between circulating line, lower circulating line;
Manage in each top set, lower circulating line is distributed with some apertures;
The mouth of pipe of described 2 reactant pan feeding pipelines circularized all stretches out outside cylindrical shell.
Further, compound interleave cloth liquid reactor as above, is provided with the filter course of one deck for being filtered in cylindrical shell by pellet type catalyst at the reactant outlet area of cylindrical shell.
Further, compound interleave cloth liquid reactor as above, described filter course is the Cylinder wall structure of a ring-type, and and leaves certain interval between cylinder inboard wall.。
Further, compound interleave cloth liquid reactor as above, is distributed with some reactant liquid outlets in the surrounding of cylindrical shell, and all reactant liquid outlets are all arranged in the regional extent that filter course covers.
Further, compound interleave cloth liquid reactor as above, described reactant liquid outlet is evenly distributed on cylindrical shell circumferentially.
Further, compound interleave cloth liquid reactor as above, in cylindrical shell, be provided with the snakelike cooling coil of ring-type, and the snakelike cooling coil of this ring-type is the concentric structure that multiple ring is formed, cooling liquid outlet and the cooling fluid entrance of this snakelike cooling coil all stretch out outside cylindrical shell.
Further, compound interleave cloth liquid reactor as above, arranges one deck outer cylinder body in the periphery of described cylindrical shell, is formed with gap between this outer cylinder body and cylindrical shell, in this gap, be provided with spiral guide plate.
The compound interleave cloth liquid reactor that the utility model provides, owing to being provided with compound interleave liquid distributor in cylindrical shell, this compound interleave liquid distributor not only increases cloth liquid zone, and the alternate alternately cloth of reaction liquid is gone out, the instantaneous reactant liquor that just can make fully mixes, thus shorten incorporation time, thus make reaction more abundant, improve the production efficiency of product.
Accompanying drawing explanation
Fig. 1 is the utility model compound interleave cloth liquid structure of reactor figure;
Fig. 2 is the utility model compound interleave liquid distributor structural representation;
Fig. 3 is that the B-B of Fig. 2 is to sectional view;
Fig. 4 is the lateral structural representation of reactant pan feeding pipeline;
Fig. 5 is that the C-C of Fig. 4 is to sectional view;
Fig. 6 is that the D-D of Fig. 1 is to sectional view.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearly, below technical scheme in the utility model be clearly and completely described, obviously, described embodiment is the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Embodiment 1:
The compound interleave cloth liquid reactor that the utility model provides, comprises cylindrical shell 1, in described cylindrical shell 1, is provided with compound interleave liquid distributor 2; Described compound interleave liquid distributor comprises: at least 2 reactant pan feeding pipelines, each reactant pan feeding pipeline is communicated with some laterals, together with the lateral of each reactant pan feeding pipeline is arranged evenly with the lateral interleaved of other reactant pan feeding pipeline, each lateral is distributed with some apertures; The mouth of pipe of all reactant pan feeding pipelines all stretches out outside cylindrical shell 1.
Particularly, the compound interleave cloth liquid reactor that the utility model provides, owing to being provided with compound interleave liquid distributor 2 in cylindrical shell 1, this compound interleave liquid distributor has two reactant pan feeding pipelines at least, during use, different reactant liquids is dropped into from different reactant pan feeding pipelines, then reactant liquid is from the aperture ejection respective lateral, due to the lateral of each reactant pan feeding pipeline arranged evenly with the lateral interleaved of other reactant pan feeding pipeline together with, therefore, all reactant liquids just can instantaneous mutual mixing, thus make all liquid reactants can instantaneous mixing abundant, thus shorten incorporation time, improve the production efficiency of product, in addition on the one hand, this compound interleave liquid distributor increases cloth liquid zone, therefore makes reaction more abundant.
Embodiment 2:
The present embodiment is on the basis of embodiment 1, giving one can by two kinds of sufficient compound interleave liquid distributor of the instantaneous mixing of liquid reactions material, as shown in Figure 2 and Figure 3, this compound interleave liquid distributor comprises 2 reactant pan feeding pipelines circularized, be respectively circulating line 22, lower circulating line 21, upper circulating line 22 is communicated with some top sets pipe 221, be communicated with some inferior division pipes 211 at lower circulating line 21, described top set pipe 221 and inferior division pipe 211 interleaved are distributed between circulating line 22, lower circulating line 21; As shown in Figure 4, Figure 5, each top set pipe 221, inferior division pipe 211 are distributed with some apertures;
The mouth of pipe (namely going up material inlet 222, lower material inlet 212) of described 2 reactant pan feeding pipelines circularized all stretches out at cylindrical shell 1 outer (as shown in Figure 1).
In the present embodiment, as shown in Figure 1, reaction mass drops into from upper material inlet 222, lower material inlet 212 respectively, then reaction mass carries out staggered mixing through the branched pipe of compound interleave liquid distributor in cylindrical shell 1, granular catalyst enters in cylindrical shell 1 from catalyst inlet 8 simultaneously, then, under the effect of agitator 9, catalyst is suspended in reactant equably reaction is carried out smoothly.
Embodiment 3:
The present embodiment is on the basis of embodiment 1 or 2, and done further improvement, improvements are: the reactant outlet area of cylindrical shell 1 is provided with the filter course 3 of one deck for being filtered in cylindrical shell by pellet type catalyst.
Particularly, in order to prevent catalyst residue outflow tube and affect purity, the quality of product together with product, the utility model is every on cylindrical shell 1 place arranging reactant outlet, is all coated with one deck catalyst filtration layer.
Embodiment 4:
The present embodiment, on the basis of embodiment 3, has done further improvement to the structure of described filter course 3, and namely filter course 3 is the Cylinder wall structure of a ring-type, leaves certain gap between this filter course 3 and inside of cylindrical shell 1.
In order to reactor preparation technology simplifies, do not need the ground only having reactant to export that filter course is set just now, but directly to placing the Cylinder wall structure filter course of a ring-type in cylindrical shell 1, so no matter where reactant outlet is arranged on cylinder lateral wall, this filter course can play the effect of filtering catalyst, described filter course is the stainless steel cylinder having the sponge shape of micropore made with sintering process, the inwall of this stainless steel cylinder and cylindrical shell 1 has a distance, and this distance will ensure that flow section matches with outlet caliber.
Embodiment 5:
The present embodiment is on the basis of embodiment 3 or 4, and done further improvement, improvements are, is distributed with some reactant liquid outlets 4 in the surrounding of cylindrical shell 1, and all reactant liquid outlets 4 are all arranged in the regional extent that filter course 3 covers.
The compound interleave cloth liquid reactor that the present embodiment provides, cylindrical shell 1 is provided with several reactant liquid outlets 4, its objective is the outlet area of augmenting response thing, reactant reflect mouth region be inhaled into outlet Anywhere time flow velocity evenly and slowly, thus the component content of outlets products is made substantially to be consistent, can not form the heap sum blocking of local catalyst, the catalyst be blocked is followed with ring together by the liquid stream that stirs at any time.
Embodiment 6:
As shown in Figure 1 and Figure 6, the present embodiment is on the basis of embodiment 5, further improvement has been done to reactant liquid outlet 4, namely enclose circumferentially at one of cylindrical shell 1, uniform parts has 9 reactant liquid outlets 4, and each reactant liquid outlet 4 is distributed with 3 reactant outlets in the vertical, totally 27 reactant liquid outlets, as shown in Figure 1, each reactant liquid outlet 4 comprises: the first reactant outlet 41, second reactant outlet the 42, the 3rd reactant outlet 43, all reactant outlets are evenly distributed on cylindrical shell 1 circumferentially.
The present embodiment adopts multiple spot export structure, and all outlet ports is evenly distributed on cylindrical shell, and advantage is that outlet area suction flow velocity is everywhere tending towards evenly with slow.
Embodiment 7:
The present embodiment is on the basis of above-mentioned any embodiment, as shown in Figure 5, add following cooling structure: the snakelike cooling coil 5 being provided with ring-type in cylindrical shell 1, and the snakelike cooling coil 5 of this ring-type is the concentric structure (the present embodiment adopts 2 layers of snakelike cooling coil) that multiple ring is formed, cooling liquid outlet and the cooling fluid entrance of this snakelike cooling coil 5 all stretch out outside cylindrical shell 1.
The present embodiment is a kind of structure of novelty as cooling element at reactor inner chamber centre serpentine coil, its advantage be can according to required heat exchange area adjustment coiled pipe be between spacing, and owing to being bilayer or sandwich construction, make heat exchange more fully, evenly, thus improve the quality of product further.
Embodiment 8:
The present embodiment is on the basis of above-mentioned any embodiment, do further improvement, namely one deck outer cylinder body 6 is set in the periphery of described cylindrical shell 1, gap is formed between this outer cylinder body 6 and cylindrical shell 1, in this gap, be provided with spiral guide plate 7, outer cylinder body 6 is provided with 62, one, gas outlet air inlet 61.
The effect of described outer cylinder body 6 is that in the cylindrical shell 1 to reactor, reactant carries out heating and being incubated, or cools, and steam or cooling water enter from air inlet 61, and then fluid flows through from guide plate 7, thus make heat exchange more fast uniform and stable.
Last it is noted that above embodiment is only in order to illustrate the technical solution of the utility model, be not intended to limit; Although be described in detail the utility model with reference to previous embodiment, those of ordinary skill in the art is to be understood that: it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein portion of techniques feature; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the spirit and scope of each embodiment technical scheme of the utility model.
Claims (9)
1. a compound interleave cloth liquid reactor, is characterized in that, comprises cylindrical shell (1), it is characterized in that, is provided with compound interleave liquid distributor (2) in described cylindrical shell (1);
Described compound interleave liquid distributor comprises: at least 2 reactant pan feeding pipelines, each reactant pan feeding pipeline is communicated with some laterals, together with the lateral of each reactant pan feeding pipeline is arranged evenly with the lateral interleaved of other reactant pan feeding pipeline, each lateral is distributed with some apertures;
The mouth of pipe of all reactant pan feeding pipelines all stretches out at cylindrical shell (1) outward.
2. compound interleave cloth liquid reactor according to claim 1, it is characterized in that, comprise 2 reactant pan feeding pipelines circularized, be respectively circulating line (22), lower circulating line (21), upper circulating line (22) is communicated with some top sets pipe (221), be communicated with some inferior division pipes (211) at lower circulating line (21), described top set's pipe (221) and inferior division pipe (211) interleaved are distributed between circulating line (22), lower circulating line (21);
At each top set's pipe (221), inferior division pipe, (211) are distributed with some apertures;
The mouth of pipe of described 2 reactant pan feeding pipelines circularized all stretches out at cylindrical shell (1) outward.
3. compound interleave cloth liquid reactor according to claim 1 and 2, is characterized in that, the reactant outlet area of cylindrical shell (1) is provided with the filter course (3) of one deck for being filtered in cylindrical shell by pellet type catalyst.
4. compound interleave cloth liquid reactor according to claim 3, is characterized in that, described filter course (3) is the Cylinder wall structure of a ring-type, and and leaves certain interval between cylindrical shell (1) inwall.
5. compound interleave cloth liquid reactor according to claim 4, it is characterized in that, be distributed with some reactant liquid outlets (4) in the surrounding of cylindrical shell (1), all reactant liquid outlets (4) are all arranged in the regional extent that filter course (3) covers.
6. compound interleave cloth liquid reactor according to claim 5, is characterized in that, described reactant liquid outlet (4) is evenly distributed on cylindrical shell (1) circumferentially.
7. according to the compound interleave cloth liquid reactor of claim 1 or 2, it is characterized in that, the snakelike cooling coil (5) of ring-type is provided with in cylindrical shell (1), and the concentric structure that the snakelike cooling coil (5) of this ring-type is formed for multiple ring, the cooling liquid outlet of this snakelike cooling coil (5) and cooling fluid entrance all stretch out at cylindrical shell (1) outward.
8. compound interleave cloth liquid reactor according to claim 3, it is characterized in that, the snakelike cooling coil (5) of ring-type is provided with in cylindrical shell (1), and the concentric structure that the snakelike cooling coil (5) of this ring-type is formed for multiple ring, the cooling liquid outlet of this snakelike cooling coil (5) and cooling fluid entrance all stretch out at cylindrical shell (1) outward.
9. compound interleave cloth liquid reactor according to claim 3, it is characterized in that, in the periphery of described cylindrical shell (1), one deck outer cylinder body (6) is set, be formed with gap between this outer cylinder body (6) and cylindrical shell (1), in this gap, be provided with spiral guide plate (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520130886.1U CN204503036U (en) | 2015-03-07 | 2015-03-07 | Compound interleave cloth liquid reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520130886.1U CN204503036U (en) | 2015-03-07 | 2015-03-07 | Compound interleave cloth liquid reactor |
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| Publication Number | Publication Date |
|---|---|
| CN204503036U true CN204503036U (en) | 2015-07-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520130886.1U Expired - Fee Related CN204503036U (en) | 2015-03-07 | 2015-03-07 | Compound interleave cloth liquid reactor |
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| CN (1) | CN204503036U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107195942A (en) * | 2016-03-14 | 2017-09-22 | 大连融科储能技术发展有限公司 | Electrolyte storage tank, flow battery, box flow battery system and flow battery charge/discharge control method |
| CN107403937A (en) * | 2017-08-18 | 2017-11-28 | 上海电气集团股份有限公司 | Electrolyte suction apparatus and the electrolyte storage tank for including it |
| CN114534657A (en) * | 2022-03-02 | 2022-05-27 | 重庆东庚工程技术有限公司 | Microchannel fast reactor |
-
2015
- 2015-03-07 CN CN201520130886.1U patent/CN204503036U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107195942A (en) * | 2016-03-14 | 2017-09-22 | 大连融科储能技术发展有限公司 | Electrolyte storage tank, flow battery, box flow battery system and flow battery charge/discharge control method |
| CN107403937A (en) * | 2017-08-18 | 2017-11-28 | 上海电气集团股份有限公司 | Electrolyte suction apparatus and the electrolyte storage tank for including it |
| CN107403937B (en) * | 2017-08-18 | 2024-02-06 | 上海电气(安徽)储能科技有限公司 | Electrolyte suction device and electrolyte storage tank comprising same |
| CN114534657A (en) * | 2022-03-02 | 2022-05-27 | 重庆东庚工程技术有限公司 | Microchannel fast reactor |
| CN114534657B (en) * | 2022-03-02 | 2023-08-08 | 重庆东庚工程技术有限公司 | Microchannel rapid reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150729 Termination date: 20160307 |